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JPH0760024B2 - Refrigeration equipment - Google Patents
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JPH0760024B2 - Refrigeration equipment - Google Patents

Refrigeration equipment

Info

Publication number
JPH0760024B2
JPH0760024B2 JP32660988A JP32660988A JPH0760024B2 JP H0760024 B2 JPH0760024 B2 JP H0760024B2 JP 32660988 A JP32660988 A JP 32660988A JP 32660988 A JP32660988 A JP 32660988A JP H0760024 B2 JPH0760024 B2 JP H0760024B2
Authority
JP
Japan
Prior art keywords
refrigerant
temperature
frequency
reservoir
boiling point
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP32660988A
Other languages
Japanese (ja)
Other versions
JPH02171556A (en
Inventor
邦泰 内山
伸二 渡辺
章 藤高
宏治 室園
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP32660988A priority Critical patent/JPH0760024B2/en
Publication of JPH02171556A publication Critical patent/JPH02171556A/en
Publication of JPH0760024B2 publication Critical patent/JPH0760024B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、混合冷媒を用いた冷凍装置に関するものであ
る。
Description: TECHNICAL FIELD The present invention relates to a refrigerating apparatus using a mixed refrigerant.

従来の技術 混合冷媒を用いた冷凍装置は、そのサイクル内部を循環
する冷媒の組成比率を可変とすることにより、能力制御
や性能改善を行なうことができる。
2. Description of the Related Art A refrigeration system using a mixed refrigerant can perform capacity control and performance improvement by varying the composition ratio of the refrigerant circulating inside the cycle.

従来、特に非共沸混合冷媒を用いた冷凍装置のサイクル
内部を循環する冷媒組成を可変とする方式として、沸点
の違いを利用した精留分離方式が用いられている(例え
ば特開昭62−280556号公報)。
Conventionally, a rectification separation system utilizing a difference in boiling point has been used as a system for varying the composition of a refrigerant circulating in a cycle of a refrigeration system using a non-azeotropic mixed refrigerant (for example, JP-A-62- 280556 publication).

以下第11図を参照しながら、精留分離方式を用いた冷凍
装置の一例について説明する。
An example of the refrigerating apparatus using the rectification separation system will be described below with reference to FIG.

第11図は従来例を示す冷凍サイクル図である。FIG. 11 is a refrigeration cycle diagram showing a conventional example.

第11図において、1は圧縮機、2は四方弁、3は室外熱
交換器、4は主回路用減圧器、5は室内熱交換器で環状
に接続されて主回路を構成している。また室外熱交換器
3と減圧器4の中間と、精留塔6の底部ともに加熱器7
を貫通し逆止弁8を介して接続するとともに加熱器7と
逆止弁8に並列に第一の減圧器9を設け、また逆止弁8
と精留塔6の底部との中間と冷媒貯留器10の底部とを電
磁開閉弁11を介して接続し、また室内熱交換器5と主回
路の減圧器4の中間と精留塔6の底部とを加熱器7を貫
通し逆止弁12を介して接続するとともに加熱器7と逆止
弁12に並列に減圧器13を設け、さらに精留塔6の頂部と
冷媒貯留器10の頂部とを冷却器14を貫通し、精留塔6の
頂部と冷媒貯留器10の底部とを接続している。なお本従
来例における冷媒は沸点差を有する2種類の冷媒からな
る非共沸混合冷媒を用いる。
In FIG. 11, 1 is a compressor, 2 is a four-way valve, 3 is an outdoor heat exchanger, 4 is a main circuit decompressor, and 5 is an indoor heat exchanger, which are annularly connected to form a main circuit. The heater 7 is provided both in the middle of the outdoor heat exchanger 3 and the decompressor 4 and at the bottom of the rectification column 6.
Through the check valve 8 and connected via a check valve 8 and a first pressure reducer 9 is provided in parallel with the heater 7 and the check valve 8;
And the bottom of the rectification tower 6 and the bottom of the refrigerant reservoir 10 are connected via an electromagnetic on-off valve 11, and also between the indoor heat exchanger 5 and the decompressor 4 of the main circuit and the rectification tower 6. The bottom part is connected to the bottom part through the heater 7 via the check valve 12, and the decompressor 13 is provided in parallel with the heater 7 and the check valve 12, and the top part of the rectification column 6 and the top part of the refrigerant reservoir 10 are provided. Through the cooler 14 to connect the top of the rectification column 6 and the bottom of the refrigerant reservoir 10. As the refrigerant in this conventional example, a non-azeotropic mixed refrigerant composed of two kinds of refrigerants having different boiling points is used.

以上のように構成された冷凍装置について、以下その動
作について説明する。
The operation of the refrigerating apparatus configured as described above will be described below.

暖房運転時、室内温度センサーで検出した室内温度を設
定温度と比較し設定温度より高い場合、冷媒は第11図の
実線の矢印のように流れ、電磁開閉弁11はこの時開いて
いるため、冷媒貯留器10の中の冷媒組成は主回路と同じ
であり、高沸点成分と低沸点成分の混合した状態で高能
力が得られる。
During heating operation, when the indoor temperature detected by the indoor temperature sensor is compared with the set temperature and is higher than the set temperature, the refrigerant flows as shown by the solid line arrow in FIG. 11, and the solenoid on-off valve 11 is open at this time. The composition of the refrigerant in the refrigerant reservoir 10 is the same as that of the main circuit, and high capacity is obtained in the state where the high boiling point component and the low boiling point component are mixed.

一方、室内温度が上昇して設定温度より高くなると、電
磁開閉弁11が閉じて冷媒は点線の矢印のように流れる。
室内熱交換器5を出た過冷却のとれた冷媒の一部は、加
熱器7へ入り吐出ガスにより加熱されガス成分を発生さ
せて精留塔6に入る。精留塔6に入った冷媒のガス成分
は塔中を上昇していき冷却器14に入り、ここで吸入ガス
により冷却液化され冷媒貯留器10に導かれ、その一部は
精留塔の頂部に還流され塔中を上昇してくるガス成分と
気液接触を行い物質移動および熱交換を行う。このサイ
クルを繰り返すことにより冷媒貯留器10の中の冷媒は低
沸点成分が多くなり主回路を流れる冷媒の組成は高沸点
成分が多い状態になり低能力が得られる。
On the other hand, when the room temperature rises and becomes higher than the set temperature, the electromagnetic on-off valve 11 closes and the refrigerant flows as shown by the dotted arrow.
A part of the supercooled refrigerant that has exited the indoor heat exchanger 5 enters the heater 7 and is heated by the discharge gas to generate a gas component, which then enters the rectification column 6. The gas component of the refrigerant that entered the rectification tower 6 rises in the tower and enters the cooler 14, where it is cooled and liquefied by the suction gas and guided to the refrigerant reservoir 10, a part of which is the top of the rectification tower. It makes a gas-liquid contact with the gas components that are refluxed in the column and rising in the tower for mass transfer and heat exchange. By repeating this cycle, the refrigerant in the refrigerant reservoir 10 has a large amount of low-boiling components, and the composition of the refrigerant flowing through the main circuit is in a state of having a large amount of high-boiling components, so that low capacity is obtained.

発明が解決しようとする課題 しかしながら上記のようにな構成では、以下のような課
題があった。
Problems to be Solved by the Invention However, the above-described configuration has the following problems.

まず第1に本従来例では低沸点冷媒を貯留することによ
り、主回路の低沸点成分比率を低下させる場合について
述べたが、例えば暖房運転開始時の様に高暖房能力の必
要なときに高沸点冷媒をも貯留して主回路の冷媒組成比
率を広範囲に可変させるためには、分離器下部に貯留器
および加熱器を必要とするため構成が複雑になる。冷媒
が3種類以上になると分離器,加熱器,貯留器が必要と
なるため構成はさらに複雑になる。
First, in the conventional example, the case where the low boiling point component ratio of the main circuit is reduced by storing the low boiling point refrigerant has been described. In order to store the boiling point refrigerant as well and vary the composition ratio of the refrigerant in the main circuit over a wide range, a reservoir and a heater are required under the separator, which complicates the configuration. When the number of refrigerants is three or more, a separator, a heater, and a reservoir are required, which further complicates the configuration.

第2に精留分離では精留塔を垂直にしなければならない
とか、貯留器と精留塔の高さに設置上の制限がある上、
沸点差を利用したものであるため、共沸混合冷媒等の沸
点の近いものについては使用できないなど精留分離特有
の課題を有していた。
Secondly, in the rectification separation, the rectification tower must be vertical, and the height of the reservoir and the rectification tower is limited due to installation.
Since it utilizes the difference in boiling points, it has problems peculiar to rectification separation, such as azeotropic mixed refrigerants having similar boiling points cannot be used.

本発明は上記課題に鑑み、冷媒混合比率可変装置および
室内温度センサーを設け、室内温度と室内設定温度との
差により負荷を的確に検知し冷房,暖房運転において効
率よい安定した能力制御が可能な冷凍装置を提供するも
のである。
In view of the above problems, the present invention provides a refrigerant mixing ratio variable device and an indoor temperature sensor, and accurately detects a load based on a difference between an indoor temperature and an indoor set temperature to enable efficient and stable capacity control in cooling and heating operations. A refrigeration system is provided.

課題を解決するための手段 上記課題を解決するために本発明は、周波数可変装置を
具備した圧縮機,凝縮機,主絞り装置,蒸発器を環状に
接続した主回路に複数種類の冷媒を封入した冷凍サイク
ルにおいて、特定の種類の冷媒の通過を容易とする機能
膜を有する冷媒分離装置を複数個接続し、機能膜の透過
側および非透過側の冷媒分離装置を出た冷媒を任意に貯
留できる貯留器を透過側,非透過側それぞれに電磁開閉
弁と減圧装置もしくは可変式減圧装置を介して主回路に
接続して冷媒組成比率可変サイクルを構成し、室内温度
を検出する温度検出手段と、前記温度検出手段による検
出温度と室内設定温度にある値を加えた設定温度との
大,小を比較する第1の比較手段と、運転開始からの時
間経過を計測するタイマーと前記タイマーの計測値と設
定時間を比較する第2の比較手段と、前記第1の比較手
段により設定温度より小の場合で前記第2の比較手段に
より設定時間より小の場合、最も低沸点の成分以外の冷
媒が貯留器に貯留されるように切り換える第1の出力モ
ードに、また前記第1の比較手段により設定温度より小
の場合で前記第2の比較手段により設定時間より大の場
合、最も高沸点の成分の冷媒が貯留器に貯留されるよう
に切り換える第2の出力モードに、また前記第1の比較
手段により設定温度より大の場合、最も低沸点の成分の
冷媒が貯留器に貯留されるように切り換える第3の出力
モードに移行する移行手段と前記出力モードにより電磁
開閉弁もしくは可変式減圧装置に電気信号を出力する出
力手段を具備したものである。
Means for Solving the Problems In order to solve the above problems, according to the present invention, a plurality of types of refrigerants are enclosed in a main circuit in which a compressor, a condenser, a main expansion device, and an evaporator each having a variable frequency device are annularly connected. In the refrigeration cycle described above, a plurality of refrigerant separators having a functional film that facilitates passage of a specific type of refrigerant are connected, and the refrigerant that exits the refrigerant separators on the permeation side and the non-permeation side of the functional film is arbitrarily stored. A reservoir that can be connected to the main circuit via a solenoid on-off valve and a pressure reducing device or a variable pressure reducing device on the permeate side and the non-permeate side, respectively, constitutes a refrigerant composition ratio variable cycle, and temperature detecting means for detecting the room temperature. First comparison means for comparing the detected temperature by the temperature detection means and the set temperature obtained by adding a certain value to the indoor set temperature, a first comparison means, a timer for measuring the elapsed time from the start of operation, and the measurement of the timer A second comparison means for comparing a value with a set time, and a refrigerant other than the lowest boiling point component when the temperature is lower than the set temperature by the first comparison means and smaller than the set time by the second comparison means. To a first output mode for switching so as to be stored in the reservoir, and when the temperature is lower than the set temperature by the first comparison means and longer than the set time by the second comparison means, the highest boiling point In the second output mode in which the component refrigerant is switched to be stored in the reservoir, and when the temperature is higher than the set temperature by the first comparing means, the component refrigerant having the lowest boiling point is stored in the reservoir. It is provided with a transition means for transitioning to a third output mode for switching to the above and an output means for outputting an electric signal to the electromagnetic on-off valve or the variable pressure reducing device according to the output mode.

また本発明は温度検出手段による室内温度と室内設定温
度にある値を加えた設定温度との差が任意の値以上の場
合、最も高沸点の成分以外の冷媒が貯留器に貯留される
ように切り換える第4の出力モードに移行する移行手段
と前記出力モードにより電磁開閉弁もしくは可変式減圧
装置に電気信号を出力する出力手段を具備したものであ
る。
Further, the present invention, when the difference between the room temperature by the temperature detection means and the set temperature obtained by adding a certain value to the room set temperature is an arbitrary value or more, the refrigerant other than the highest boiling point component is stored in the reservoir. It is provided with a transition means for transitioning to a fourth output mode for switching and an output means for outputting an electric signal to the electromagnetic on-off valve or the variable pressure reducing device according to the output mode.

運転開始からの時間経過を計測するタイマーとこのタイ
マーの計測値と設定時間とを比較する第1の比較手段
と、圧縮機の運転周波数を検出する周波数検出手段と、
この周波数検出手段による検出周波数と設定周波数との
大、小とを比較する第2の比較手段と、前記第2の比較
手段により設定周波数より大の場合で前記第1の比較手
段により設定時間より小の場合、最も低沸点の成分以外
の冷媒が貯留器に貯留されるように切り換える第1の出
力モードに、また前記第2の比較手段により設定周波数
より大の場合で前記第1の比較手段により設定時間より
大の場合、最も高沸点の成分の冷媒が貯留器に貯留され
るように切り換える第2の出力モードに、また前記第2
の比較手段により設定周波数より小の場合、最も低沸点
の成分の冷媒が貯留器に貯留されるように切り換える第
3の出力モードに移行する移行手段と前記出力モードに
より電磁開閉弁もしくは可変式減圧装置に電気信号を出
力する出力手段を具備したものである。
A timer for measuring the passage of time from the start of operation, a first comparing means for comparing the measured value of this timer with a set time, and a frequency detecting means for detecting the operating frequency of the compressor,
Second comparing means for comparing the detected frequency of the frequency detecting means with the set frequency, and a second comparing means for comparing the set frequency with the second comparing means, and a second comparing means for comparing the set frequency with the set time. When the value is small, the first comparing mode is set in the first output mode in which the refrigerant other than the component with the lowest boiling point is switched to be stored in the reservoir, and when the frequency is higher than the set frequency by the second comparing means. When the time is longer than the set time, the second output mode is switched so that the refrigerant having the highest boiling point is stored in the reservoir, and the second output mode is set.
If the frequency is smaller than the set frequency by the comparison means of the above, the switching means is switched to the third output mode in which the refrigerant having the lowest boiling point component is stored in the reservoir, and the electromagnetic on-off valve or the variable pressure reducing valve is selected depending on the output mode. The device is provided with output means for outputting an electric signal.

作用 本発明は上記構成により、非共沸混合冷媒に限らず共沸
混合冷媒についても冷媒分離でき、冷暖房ともに負荷を
的確につかみ、必要負荷に応じて高沸点冷媒成分,中間
沸点冷媒成分または低沸点冷媒成分を分離し、冷媒混合
比率を可変させることにより幅広い効率のよい能力制御
運転を可能にするとともに分離回路の構成部品の取付設
置上の制約の解消,分離回路の小型化と簡素化を図るこ
とができる。
Effect The present invention, by the above configuration, can separate refrigerant not only for non-azeotropic mixed refrigerants but also for azeotropic mixed refrigerants, accurately grasp the load in both cooling and heating, and depending on the required load, high boiling point refrigerant component, intermediate boiling point refrigerant component or low boiling point refrigerant component. By separating the boiling point refrigerant components and varying the refrigerant mixing ratio, a wide range of highly efficient capacity control operation is possible, while eliminating the restrictions on the installation and installation of the components of the separation circuit, and reducing the size and simplification of the separation circuit. Can be planned.

実施例 以下前記機能膜を用いた冷凍サイクルの実施例について
第1図を参考に説明する。
Example An example of a refrigeration cycle using the functional film will be described below with reference to FIG.

第1図に、冷媒として、R−22,R−12とR−13B1の非共
沸混合冷媒を用いた場合の一実施例を、第2図に機能膜
を用いた冷媒分離器(以下分離器という)の一実施例を
示す。
FIG. 1 shows an embodiment in which a non-azeotropic mixed refrigerant of R-22, R-12 and R-13B1 is used as the refrigerant, and FIG. 2 shows a refrigerant separator using a functional film (hereinafter referred to as “separator”). (Referred to as a container).

第1図において、21は圧縮機、22は凝縮機、23は主絞り
装置、24は蒸発器で順次環状に接続されて主回路を構成
している。冷媒R−12成分を透過しやすく、他の成分を
透過しにくい機能膜103を備えた第1の分離器101の入口
配管105は主絞り装置23の手前の高圧側へ接続され、出
口配管106は冷媒R−22成分を透過しやすく他の成分を
透過しにくい機能膜103′を備えた第2の分離器101′の
入口に接続され、出口配管106′は貯留器25,第1の絞り
装置26を介して前記主絞り装置23の後の低圧側へ接続さ
れている。一方、分離器内部は第2図に示すように例え
ば分離器101′では分離器本体102を網状の保持具104で
高圧側空間a,低圧側空間bに仕切り、保持具104の高圧
側にジメチルシリコンの薄膜を用いた前記機能膜103を
設置する。また第1の分離器101,第2の分離器101′の
透過冷媒出口配管107,107′はそれぞれ貯留器27,28、第
3の絞り装置29、第4の絞り装置30を介して前記主絞り
装置23の後の低圧側へ接続されている。また透過冷媒出
口配管107,107′はそれぞれ冷却器31,32と熱交換的に接
続されている。
In FIG. 1, reference numeral 21 is a compressor, 22 is a condenser, 23 is a main expansion device, and 24 is an evaporator, which are sequentially connected in an annular shape to form a main circuit. The inlet pipe 105 of the first separator 101, which is provided with the functional film 103 that allows the refrigerant R-12 component to easily pass therethrough and hardly allows other components to pass therethrough, is connected to the high pressure side in front of the main expansion device 23, and the outlet pipe 106. Is connected to the inlet of a second separator 101 'equipped with a functional film 103' which allows the R-22 component to pass easily and other components to pass less, and the outlet pipe 106 'has a reservoir 25 and a first throttle. It is connected via a device 26 to the low pressure side after the main throttle device 23. On the other hand, inside the separator, as shown in FIG. 2, for example, in the separator 101 ′, the separator main body 102 is partitioned into a high pressure side space a and a low pressure side space b by a mesh-shaped holder 104, and a high pressure side of the holder 104 is filled with dimethyl. The functional film 103 using a thin film of silicon is installed. Further, the permeated refrigerant outlet pipes 107, 107 'of the first separator 101, the second separator 101' are connected to the main throttle device via the reservoirs 27, 28, the third throttle device 29, and the fourth throttle device 30, respectively. It is connected to the low voltage side after 23. Further, the permeated refrigerant outlet pipes 107, 107 'are connected to the coolers 31, 32 by heat exchange.

ここで第3図に示すブロック回路と第4図に示す制御回
路の関係について説明すると、第4図に示す室内温度セ
ンサー33は第3図に示す室内温度検出手段に相当し、第
4図に示すコンパレータ34は第3図の第1の比較手段に
相当し、第4図のマイクロコンピュータ35は第3図のタ
イマー計測値と設定時間を比較する第2の比較手段およ
び移行手段に相当し、第4図の出力回路36は第3図の出
力手段に相当している。
Explaining the relationship between the block circuit shown in FIG. 3 and the control circuit shown in FIG. 4, the indoor temperature sensor 33 shown in FIG. 4 corresponds to the indoor temperature detecting means shown in FIG. The comparator 34 shown corresponds to the first comparing means in FIG. 3, and the microcomputer 35 in FIG. 4 corresponds to the second comparing means and shifting means for comparing the timer measured value with the set time in FIG. The output circuit 36 shown in FIG. 4 corresponds to the output means shown in FIG.

以上のように構成された制御回路の動作について、第1
図から第4図を参考に説明する。
Regarding the operation of the control circuit configured as described above,
It will be described with reference to FIGS.

暖房運転時、室内温度を室内温度センサー33で検出しそ
れを室内設定温度にある値を加えた設定温度とコンパレ
ータ34で比較し設定温度より低く、かつ暖房運転開始よ
りの時間経過を計測するタイマーの値が設定時間よりも
少ない場合、第2の絞り装置29、第3の絞り装置30の弁
開度を小さくすることにより、機能膜103を透過しやす
いR−12は冷却器31により冷却されて液冷媒で貯留器27
に貯留される。一方、機能膜103を透過しにくいR−22,
R−13B1は出口配管106を出て第2の分離器101′に入
る。機能膜103′を透過しやすいR−22は冷却器32によ
り冷却されて液冷媒で貯留器28に貯留される。他方機能
膜103′を透過しにくいR−13B1は出口配管1O6′を出て
貯留器25、第1の絞り装置26を介して主絞り装置23の後
の低圧側へ送られる。従って、主回路のR−12,R−22比
率は低下し、R−13B1比率が上昇して最も高能力が得ら
れる。
During heating operation, a timer that detects the indoor temperature with the indoor temperature sensor 33, compares it with the set temperature that is a certain value added to the indoor set temperature with the comparator 34, is lower than the set temperature, and measures the elapsed time from the start of the heating operation. When the value of is less than the set time, the valve openings of the second expansion device 29 and the third expansion device 30 are reduced so that R-12, which easily penetrates the functional film 103, is cooled by the cooler 31. Liquid refrigerant reservoir 27
Stored in. On the other hand, R-22, which is difficult to pass through the functional film 103,
R-13B1 exits the outlet pipe 106 and enters the second separator 101 '. The R-22 that easily permeates the functional film 103 'is cooled by the cooler 32 and stored in the reservoir 28 as a liquid refrigerant. On the other hand, R-13B1 which hardly permeates the functional film 103 'exits the outlet pipe 1O6' and is sent to the low pressure side after the main expansion device 23 via the reservoir 25 and the first expansion device 26. Therefore, the R-12 and R-22 ratios of the main circuit are lowered and the R-13B1 ratio is increased to obtain the highest performance.

一方、検出温度が設定温度よりも低く、かつ暖房運転開
始よりの時間経過を計測するタイマーの値が設定時間よ
りも大きい場合、第2の絞り装置29の弁開度を小さくす
ることにより、機能膜103を透過しやすいR−12は冷却
器31により冷却されて液冷媒で貯留器27に貯留される。
一方、機能膜103を透過しにくいR22,R−13B1は出口配管
106を出て第2の分離器101′に入る。機能膜103′を透
過しやすいR−22は、冷却器32により冷却されて液冷媒
で貯留器28に入るが、ほとんど貯留されずに第3の絞り
装置30により、減圧されて主絞り装置23の後の低圧側へ
送られる。他方機能103′を透過しにくいR−13B1は出
口配管106′を出て貯留器25,第1の絞り装置26を介して
主絞り装置23の後の低圧側へ送られる。従って、主回路
のR−12比率のみが低下する。
On the other hand, when the detected temperature is lower than the set temperature and the value of the timer that measures the elapsed time from the start of the heating operation is larger than the set time, the valve opening of the second expansion device 29 is reduced to function. The R-12 that easily permeates the membrane 103 is cooled by the cooler 31 and stored in the reservoir 27 as a liquid refrigerant.
On the other hand, R22 and R-13B1 which are difficult to penetrate the functional film 103 are outlet pipes.
Exit 106 and enter second separator 101 '. The R-22, which easily permeates the functional film 103 ', is cooled by the cooler 32 and enters the reservoir 28 as a liquid refrigerant, but is hardly stored and is decompressed by the third throttle device 30 to be the main throttle device 23. Sent to the low pressure side after. On the other hand, the R-13B1 which is less likely to pass through the function 103 'exits the outlet pipe 106' and is sent to the low pressure side after the main expansion device 23 via the reservoir 25 and the first expansion device 26. Therefore, only the R-12 ratio of the main circuit is reduced.

次に室内温度が上昇して設定温度よりも高くなると、第
1の絞り装置26の弁開度を小さくする。そこで、機能膜
103を透過しやすいR−12は冷却器31により冷却されて
液冷媒で貯留器27に入るが、ほとんど貯留されずに第3
の絞り装置29により、減圧されて主絞り装置23の後の低
圧側へ送られる。一方、機能膜103を透過しにくいR22,R
−13B1は出口配管106を出て第2の分離器101′に入る。
機能膜103′を透過しやすいR−22は、R−12と同様に
して第2の絞り装置29により、減圧されて主絞り装置23
の後の低圧側へ送られる。他方機能膜103′を透過しに
くいR−13B1は出口配管106′を出て液冷媒で貯留器25
に貯留される。従って、主回路のR−13B1比率のみが低
下し、R−12,R−22比率が上昇して能力および消費電力
とも小さくなり効率のよい能力制御ができる。冷房運転
時においても同様である。
Next, when the room temperature rises and becomes higher than the set temperature, the valve opening degree of the first expansion device 26 is reduced. So, functional film
R-12, which easily passes through 103, is cooled by the cooler 31 and enters the reservoir 27 as a liquid refrigerant, but is hardly retained and the R-12
The pressure is reduced by the expansion device 29 and is sent to the low pressure side after the main expansion device 23. On the other hand, R22, R that is difficult to penetrate through the functional film 103
-13B1 exits the outlet pipe 106 and enters the second separator 101 '.
The R-22, which easily passes through the functional film 103 ', is decompressed by the second diaphragm device 29 in the same manner as the R-12, and the main diaphragm device 23.
Sent to the low pressure side after. On the other hand, R-13B1 which is difficult to permeate the functional film 103 'exits the outlet pipe 106' and is stored as a liquid refrigerant in the reservoir 25.
Stored in. Therefore, only the R-13B1 ratio of the main circuit decreases, the R-12 and R-22 ratios increase, and both the capacity and the power consumption decrease, and efficient capacity control can be performed. The same is true during the cooling operation.

以上のように本実施例によれば、室内温度センサー33を
設け室内温度と設定温度との比較および運転開始時より
の時間経過と設定時間の比較により、混合冷媒の比率を
可変して、運転開始時のように最も負荷が大きく高能力
を必要とする場合には、高沸点成分および中間沸点成分
の冷媒が分離貯留され、主回路の冷媒は低沸点成分の多
い状態になり最も高能力を得ることができ、運転開始時
以外で負荷が高い場合には高沸点成分の冷媒のみが分離
貯留され主回路の冷媒は低沸点成分と中間沸点成分の多
い状態になり高能力を得ることができ、また負荷が小さ
く低能力で十分な場合には低沸点成分が分離貯留され主
回路の冷媒は中間沸点成分および高沸点成分の多い状態
になり低能力、低消費電力を得ることができ効率のよい
能力制御を容易かつ、分離回路の構成部品の取付上の制
約のない小型化および簡素化を図った分離回路て実現で
きる。
As described above, according to the present embodiment, the indoor temperature sensor 33 is provided, and the ratio of the mixed refrigerant is changed by comparing the indoor temperature and the set temperature and comparing the elapsed time and the set time from the start of the operation. When the load is the largest and high capacity is required as at the start, the refrigerants of high boiling point component and intermediate boiling point component are separated and stored, and the refrigerant in the main circuit has a lot of low boiling point components and the highest capacity. When the load is high except when starting operation, only the high-boiling point refrigerant is separated and stored, and the main circuit refrigerant has a large amount of low-boiling point components and intermediate-boiling point components, and high performance can be obtained. When the load is small and low capacity is sufficient, the low boiling point components are separated and stored, and the refrigerant in the main circuit is in a state where there are many intermediate boiling point components and high boiling point components, and low capacity and low power consumption can be obtained, and Good ability control easy , Can be realized Te separation circuit downsized without constraints on the mounting of the components of the separation circuit and simplify.

次に、第1図,第4図,第6図により、本発明の第2の
実施例について説明する。
Next, a second embodiment of the present invention will be described with reference to FIGS. 1, 4, and 6.

ここで、第1の実施例と同一のものについては、同一の
符号を付して説明を省略する。
Here, the same components as those in the first embodiment are designated by the same reference numerals and the description thereof will be omitted.

室内温度センサー33は第6図に示す室内温度検出手段に
相当し、第4図に示すコンパレータ34は第6図の第1の
比較手段に相当している。
The indoor temperature sensor 33 corresponds to the indoor temperature detecting means shown in FIG. 6, and the comparator 34 shown in FIG. 4 corresponds to the first comparing means shown in FIG.

上記構成において、例えば暖房運転時、50℃以上の高温
度設定された場合、第1の絞り装置26、第3の絞り装置
30の弁開度を小さくすることにより、機能膜103わ透過
しやすいR−12は冷却器31により冷却されて液冷媒で貯
留器27に入るが、ほとんど貯留されずに第2の絞り装置
29により、減圧されて主絞り装置23の後の低圧側へ送ら
れる。一方、機能膜103を透過しにくいR22,R−13B1は出
口配管106を出て第2の分離器101′に入る。機能膜10
3′を透過しやすいR−22は、冷却器32により冷却され
て液冷媒で貯留器28に貯留される。他方機能膜103′を
透過しにくいR−13B1は出口配管106′を出て液冷媒で
貯留器25に貯留される。従って、主回路のR−22,R−13
B1比率が低下し、R−12比率が上昇して高温度運転が可
能となる。これはたとえば給湯運転において、給湯の温
度を上昇させる場合も同様である。
In the above configuration, for example, when a high temperature of 50 ° C. or higher is set during heating operation, the first expansion device 26 and the third expansion device 26
By reducing the valve opening of 30, the R-12, which is easily permeated through the functional film 103, is cooled by the cooler 31 and enters the reservoir 27 as a liquid refrigerant, but is hardly stored and the second throttle device is not stored.
The pressure is reduced by 29 and sent to the low pressure side after the main expansion device 23. On the other hand, R22 and R-13B1 which are less likely to permeate the functional membrane 103 exit the outlet pipe 106 and enter the second separator 101 '. Functional membrane 10
R-22, which easily passes through 3 ', is cooled by the cooler 32 and stored in the reservoir 28 as a liquid refrigerant. On the other hand, R-13B1 which hardly permeates the functional film 103 'exits the outlet pipe 106' and is stored in the reservoir 25 as a liquid refrigerant. Therefore, R-22 and R-13 of the main circuit
The B1 ratio decreases and the R-12 ratio increases, enabling high temperature operation. This also applies to the case of raising the temperature of hot water supply in hot water supply operation, for example.

以上のように本実施例によれば、高温風吹き出しのよう
に室内温度センサー33による室内温度と設定温度とを比
較して、その差が任意の値以上になったときには、低沸
点成分および中間沸点成分の冷媒が分離貯留され、主回
路の冷媒は高沸点成分の多い状態になり最も高温度を得
ることができる。
As described above, according to the present embodiment, the indoor temperature by the indoor temperature sensor 33 is compared with the set temperature like a hot air blow, and when the difference is more than an arbitrary value, the low boiling point component and the intermediate temperature are set. The refrigerant of the boiling point component is separated and stored, and the refrigerant in the main circuit has a large amount of the high boiling point component, so that the highest temperature can be obtained.

さらに、第1図,第8図,第9図により、本発明の第3
の実施例について説明する。
Furthermore, referring to FIG. 1, FIG. 8 and FIG.
An example will be described.

ここで、さきの実施例と同一のものについては、同一の
符号を付して説明を省略する。
Here, the same components as those in the previous embodiment are designated by the same reference numerals and the description thereof will be omitted.

第8図に示す周波数検出装置37は第9図に示す周波数検
出手段に相当しており、圧縮機の運転周波数を検出す
る。
The frequency detection device 37 shown in FIG. 8 corresponds to the frequency detection means shown in FIG. 9 and detects the operating frequency of the compressor.

上記構成において、暖房運転時、圧縮機運転周波数を周
波数検出装置37で検出しそれを設定周波数とコンパレー
タ34で比較し設定周波数より高く、かつ暖房運転開始よ
りの時間経過を計測するタイマーの値が設定時間よりも
少ない場合、第2の絞り装置29、第3の絞り装置30の弁
開度を小さくすることにより、機能膜103を透過しやす
いR−12は冷却器31により冷却されて液冷媒で貯留器27
に貯留される。一方、機能膜103を透過しにくいR22,R−
13B1は出口配管106を出て第2の分離器101′に入る。機
能膜103′を透過しやすいR−22は冷却器32により冷却
されて液冷媒で貯留器28に貯留される。他方機能膜10
3′を透過しにくいR−13B1は出口配管106′を出て貯留
器25、第1の絞り装置26を介して主絞り装置23後の低圧
側へ送られる。従って、主回路のR−12,R−22比率は低
下し、R−13B1比率が上昇して最も高能力が得られる。
In the above configuration, during the heating operation, the compressor operating frequency is detected by the frequency detection device 37 and is compared with the set frequency by the comparator 34 to be higher than the set frequency, and the value of the timer for measuring the elapsed time from the start of the heating operation. When the time is less than the set time, the valve openings of the second expansion device 29 and the third expansion device 30 are reduced, so that R-12, which easily penetrates the functional film 103, is cooled by the cooler 31 and the liquid refrigerant. In reservoir 27
Stored in. On the other hand, R22, R-
13B1 exits the outlet pipe 106 and enters the second separator 101 '. The R-22 that easily permeates the functional film 103 'is cooled by the cooler 32 and stored in the reservoir 28 as a liquid refrigerant. On the other hand, functional film 10
The R-13B1 which is less likely to pass through 3 ', exits the outlet pipe 106' and is sent to the low pressure side after the main expansion device 23 via the reservoir 25 and the first expansion device 26. Therefore, the R-12 and R-22 ratios of the main circuit are lowered and the R-13B1 ratio is increased to obtain the highest performance.

一方、検出周波数が設定周波数よりも高く、かつ暖房運
転開始よりの時間経過を計測するタイマーの値が設定時
間よりも大きい場合、第3の絞り装置29の弁開度を小さ
くすることにより、機能膜103を透過しやすいR−12は
冷却器31により冷却されて液冷媒で貯留器27に貯留され
る。一方、機能膜103を透過しにくいR22,R−13B1は出口
配管106を出て第2の分離器101′に入る。機能膜103′
わ透過しやすいR−22は、冷却器32により冷却されて液
冷媒で貯留器28に入るが、ほとんど貯留されずに第3の
絞り装置30により、減圧されて主絞り装置23の後の低圧
側へ送られる。他方機能膜103′を透過しにくいR−13B
1は出口配管106′を出て貯留器25,第1の絞り装置26を
介して主絞り装置23の後の低圧側へ送られる。従って、
主回路のR−12比率のみが低下する。
On the other hand, when the detected frequency is higher than the set frequency and the value of the timer that measures the elapsed time from the start of the heating operation is larger than the set time, the valve opening of the third expansion device 29 is reduced to The R-12 that easily permeates the membrane 103 is cooled by the cooler 31 and stored in the reservoir 27 as a liquid refrigerant. On the other hand, R22 and R-13B1 which are less likely to permeate the functional membrane 103 exit the outlet pipe 106 and enter the second separator 101 '. Functional film 103 ′
The R-22, which is easily permeated, is cooled by the cooler 32 and enters the reservoir 28 as a liquid refrigerant, but is hardly stored and is depressurized by the third throttling device 30 to a low pressure after the main throttling device 23. Sent to the side. On the other hand, R-13B is hard to penetrate through the functional film 103 '.
1 exits the outlet pipe 106 'and is sent to the low pressure side after the main expansion device 23 via the reservoir 25 and the first expansion device 26. Therefore,
Only the R-12 ratio of the main circuit is reduced.

次に周波数が減少して設定周波数よりも低くなると、第
1の絞り装置26の弁開度を小さくする。そこで機能膜10
3を透過しやすいR−12は冷却器31により冷却されて液
冷媒で貯留器27に入るが、ほとんど貯留されずに第2の
絞り装置29により、減圧されて主絞り装置23の後の低圧
側へ送られる。一方、機能膜103を透過しにくいR22,R−
13B1は出口配管106を出て第2の分離器101′に入る。機
能膜103′を透過しやすいR−22は、R−12と同様にし
て第2の絞り装置29により、減圧されて主絞り装置23の
後の低圧側へ送られる。他方機能膜103′を透過しにく
いR−13B1は出口配管106′を出て液冷媒で貯留器25に
貯留される。従って、主回路のR−13B1比率のみが低下
し、R−12,R−22比率が上昇して能力および消費電力と
も小さくなり効率のよい能力制御ができる。冷房運転時
においても同様である。
Next, when the frequency decreases and becomes lower than the set frequency, the valve opening degree of the first expansion device 26 is reduced. So functional film 10
R-12, which easily passes through 3, is cooled by the cooler 31 and enters the reservoir 27 as a liquid refrigerant, but is hardly stored and is decompressed by the second expansion device 29 to a low pressure after the main expansion device 23. Sent to the side. On the other hand, R22, R-
13B1 exits the outlet pipe 106 and enters the second separator 101 '. The R-22, which easily passes through the functional film 103 ', is decompressed by the second diaphragm device 29 in the same manner as R-12 and sent to the low pressure side after the main diaphragm device 23. On the other hand, R-13B1 which hardly permeates the functional film 103 'exits the outlet pipe 106' and is stored in the reservoir 25 as a liquid refrigerant. Therefore, only the R-13B1 ratio of the main circuit decreases, the R-12 and R-22 ratios increase, and both the capacity and the power consumption decrease, and efficient capacity control can be performed. The same is true during the cooling operation.

以上のように本実施例によれば、周波数検出装置37を設
け圧縮機運転周波数と設定周波数との比較および運転開
始時よりの時間経過と設定時間の比較により、混合冷媒
の比率を可変して運転開始時のように最も負荷が大きく
高能力を必要とする場合には、高沸点成分および中間沸
点成分の冷媒が分離貯留され、主回路の冷媒は低沸点成
分の多い状態になり最も高能力を得ることができ、運転
開始時以外で負荷が高い場合には高沸点成分の冷媒のみ
が分離貯留された主回路の冷媒は低沸点成分と中間沸点
成分の多い状態になり高能力を得ることができ、また負
荷が小さく低能力で十分な場合には低沸点成分が分離貯
留され主回路の冷媒は中間沸点成分および高沸点成分の
多い状態になり低能力,低消費電力を得ることができ効
率のよい能力制御を容易かつ、分離回路の構成品の取付
上の制約のない小型化および簡素化を図った分離回路で
実現できる。また、本実施例を分離型空気調和機に利用
した場合、制御が室外側のみで行え室内と室外の信号伝
送の必要がなく、制御構成が簡単にできる。
As described above, according to the present embodiment, the frequency detection device 37 is provided, and the ratio of the mixed refrigerant is changed by comparing the compressor operating frequency and the set frequency and comparing the elapsed time from the start of operation and the set time. When the load is the largest and high capacity is required, such as at the start of operation, the refrigerants of high boiling point component and intermediate boiling point component are separated and stored, and the refrigerant in the main circuit has a lot of low boiling point components and has the highest capacity. When the load is high except when starting operation, the refrigerant in the main circuit, in which only the high-boiling point refrigerant is separated and stored, has a large amount of low-boiling point components and intermediate-boiling point components to obtain high capacity. In addition, when the load is small and low capacity is sufficient, low boiling point components are separated and stored, and the refrigerant in the main circuit is in a state where there are many intermediate boiling point components and high boiling point components, and low capacity and low power consumption can be obtained. Efficient capacity control Easy and can be realized by separate circuits which attained without size reduction and simplification constraints on the mounting components of the separation circuit. Further, when the present embodiment is applied to the separation type air conditioner, the control can be performed only outside the room, and there is no need to transmit signals inside and outside the room, and the control structure can be simplified.

発明の効果 以上のように本発明は、周波数可変装置を具備した圧縮
機,凝縮機,主絞り装置,蒸発器を環状に接続した主回
路に複数種類の冷媒を封入した冷凍サイクルにおいて、
特定の種類の冷媒の通過を容易とする機能膜を有する冷
媒分離装置を複数個接続し、機能膜の透過側および非透
過側の冷媒分離装置を出た冷媒を任意に貯留できる貯留
器を透過側、非透過側それぞれに電磁開閉弁と減圧装置
もしくは可変式減圧装置を介して主回路に接続して冷媒
組成比率可変サイクルを構成し、室内温度を検出する温
度検出手段と、前記温度検出手段による検出温度と室内
設定温度にある値を加えた設定温度との大、小を比較す
る第1の比較手段と、運転開始からの時間経過を計測す
るタイマーと前記タイマーの計測値し設定時間を比較す
る第2の比較手段と、前記第1の比較手段により設定温
度より小の場合で前記第2の比較手段により設定時間よ
り小の場合、最も低沸点の成分以外の冷媒が貯留器に貯
留されるように切り換える第1の出力モードに、また前
記第1の比較手段により設定温度より小の場合で前記第
2の比較手段により設定時間より大の場合、最も高沸点
の成分の冷媒が貯留器に貯留されるように切り換える第
2の出力モードに、また前記第1の比較手段により設定
温度より大の場合、最も低沸点の成分の冷媒が貯留器に
貯留されるように切り換える第3の出力モードに移行す
る移行手段と前記出力モードにより電磁開閉弁もしくは
可変式減圧装置に電気信号を出力する出力手段を具備す
ることにより冷房、暖房運転とも負荷を的確につかみ、
必要負荷に応じて高沸点成分の分離あるいは混合あるい
は低沸点成分の分離を行い主回路を流れる冷媒の混合比
率を可変することにより幅広い効率のよい能力制御運転
を容易かつ、分離回路の構成部品の取付上の制約のない
小型化および簡素化を図った分離回路で実現できると言
う効果を奏する。
EFFECTS OF THE INVENTION As described above, the present invention is a refrigeration cycle in which a plurality of types of refrigerants are sealed in a main circuit in which a compressor, a condenser, a main expansion device, and an evaporator that are equipped with a frequency variable device are annularly connected,
A plurality of refrigerant separators that have a functional film that facilitates the passage of a specific type of refrigerant are connected, and the refrigerant that exits the refrigerant separators on the permeate and non-permeate sides of the functional film passes through a reservoir that can arbitrarily store the refrigerant. Side and non-permeate side each connected to the main circuit via an electromagnetic on-off valve and a pressure reducing device or a variable pressure reducing device to form a refrigerant composition ratio variable cycle, and temperature detecting means for detecting the room temperature, and the temperature detecting means. The first comparison means for comparing the detected temperature and the set temperature obtained by adding a certain value to the indoor set temperature by the first comparing means, the timer for measuring the elapsed time from the start of operation, and the measured value of the timer for setting the set time. When the temperature is lower than the set temperature by the second comparing means to be compared with the first comparing means and is shorter than the set time by the second comparing means, the refrigerant other than the component with the lowest boiling point is stored in the reservoir. To be cut off In the first output mode to be changed, and when the temperature is lower than the set temperature by the first comparing means and longer than the set time by the second comparing means, the refrigerant having the highest boiling point is stored in the reservoir. To the second output mode for switching to the above, and to the third output mode for switching so that the refrigerant having the lowest boiling point component is stored in the reservoir when the temperature is higher than the set temperature by the first comparing means. By appropriately providing a transfer means and an output means for outputting an electric signal to the electromagnetic on-off valve or the variable pressure reducing device according to the output mode, both the cooling operation and the heating operation accurately grasp the load,
By separating or mixing high boiling point components or separating low boiling point components according to the required load and varying the mixing ratio of the refrigerant flowing in the main circuit, a wide and efficient capacity control operation can be easily performed and The effect is that it can be realized by a separation circuit that is compact and simple without any restrictions on mounting.

また、温度検出手段による室内温度と室内設定温度にあ
る値を加えた設定温度との差が任意の値以上の場合、最
も高沸点の成分以外の冷媒が貯留器に貯留されるように
切り換える第4の出力モードに移行する移行手段と前記
出力モードにより電磁開閉弁もしくは可変式減圧装置に
電気信号を出力する出力手段を具備することにより、必
要に応じて最も高沸点の成分以外の冷媒の分離を行い、
主回路中の高沸点成分比率を高くすることにより高温度
運転を実現できる。
Further, when the difference between the room temperature by the temperature detection means and the set temperature obtained by adding a certain value to the room set temperature is equal to or more than an arbitrary value, the refrigerant other than the highest boiling point component is switched to be stored in the reservoir. 4 is provided with a transition means for transitioning to the output mode and an output means for outputting an electric signal to the electromagnetic on-off valve or the variable pressure reducing device according to the output mode, thereby separating the refrigerant other than the highest boiling point component as necessary. And then
High temperature operation can be realized by increasing the high boiling point component ratio in the main circuit.

さらに圧縮機の運転周波数を検出する周波数検出手段を
前記温度検出手段に代えて設けることにより、分離型空
気調和機に利用した場合、制御が室内側のみで室内と室
外の信号伝送の必要がなく、制御構成が簡単にできる効
果が得られる。
Further, by providing a frequency detecting means for detecting the operating frequency of the compressor in place of the temperature detecting means, when used in a separation type air conditioner, control is only required on the indoor side and there is no need for signal transmission inside and outside the room. The effect that the control structure can be simplified is obtained.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の実施例における冷媒サイクル図、第2
図は同分離器の詳細断面図、第3図は第1の実施例を示
すブロック図、第4図は同制御回路図、第5図は同フロ
ーチャート図、第6図は第2の実施例を示すブロック
図、第7図は同フローチャート図、第8図は第3の実施
例を示すブロック図、第9図は同制御回路図、第10図は
同フローチャート図、第11図は従来例における冷凍サイ
クル図である。 21……圧縮機、22……凝縮器、23……主絞り装置、24…
…蒸発器、25,27,28……貯留器、101,101′……分離
器、103,103′……機能膜、26,29,30……絞り装置、33
……温度センサー、34……コンパレータ、35……マイク
ロコンピュータ、36……出力回路、37……周波数検出装
置。
FIG. 1 is a refrigerant cycle diagram in an embodiment of the present invention, FIG.
FIG. 4 is a detailed sectional view of the separator, FIG. 3 is a block diagram showing a first embodiment, FIG. 4 is a control circuit diagram thereof, FIG. 5 is a flow chart diagram thereof, and FIG. 6 is a second embodiment. FIG. 7, FIG. 7 is the same flow chart, FIG. 8 is a block diagram showing the third embodiment, FIG. 9 is the same control circuit diagram, FIG. 10 is the same flow chart, and FIG. 11 is a conventional example. 2 is a refrigeration cycle diagram in FIG. 21 ... Compressor, 22 ... Condenser, 23 ... Main throttle device, 24 ...
… Evaporator, 25,27,28 …… Reservoir, 101,101 ′ …… Separator, 103,103 ′ …… Functional membrane, 26,29,30 …… Squeezing device, 33
...... Temperature sensor, 34 …… Comparator, 35 …… Microcomputer, 36 …… Output circuit, 37 …… Frequency detection device.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 室園 宏治 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (56)参考文献 特開 昭63−238367(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Koji Murozono 1006, Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (56) References JP-A-63-238367 (JP, A)

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】周波数可変装置を具備した圧縮機、凝縮
機、主絞り装置、蒸発器を環状に接続した主回路に複数
種類の冷媒を封入した冷凍サイクルにおいて、特定の種
類の冷媒の透過割合が他の冷媒の透過割合より大きい機
能膜を有した冷媒分離装置を複数個接続し、前記機能膜
の透過側及び非透過側の冷媒分離装置より出た冷媒を任
意に貯留する貯留器を透過側、非透過側各々に電磁開閉
弁と減圧装置もしくは可変式減圧装置を介して前記主回
路に接続して冷媒組成比率可変サイクルを構成し、室内
温度を検出する温度検出手段と、この温度検出手段によ
る検出温度と室内設定温度にある値を加えた設定温度と
の大、小を比較する第1の比較手段と、運転開始からの
時間経過を計測するタイマーとこのタイマーの計測値と
設定時間とを比較する第2の比較手段と、前記第1の比
較手段により設定温度より小の場合で前記第2の比較手
段により設定時間より小の場合、最も低沸点の成分以外
の冷媒が貯留器に貯留されるように切り換える第1のモ
ードに、また前記第1の比較手段により設定温度より小
の場合で前記第2の比較手段により設定時間より大の場
合、最も高沸点の成分の冷媒が貯留器に貯留されるよう
に切り換える第2の出力モードに、また前記第1の比較
手段により設定温度より大の場合、最も低沸点の成分の
冷媒が貯留器に貯留されるように切り換える第3の出力
モードに移行する移行手段と前記出力モードにより電磁
開閉弁もしくは可変式減圧装置に電気信号を出力する出
力手段を具備した冷凍装置。
1. A permeation ratio of a specific type of refrigerant in a refrigeration cycle in which a plurality of types of refrigerant are enclosed in a main circuit in which a compressor, a condenser, a main expansion device, and an evaporator equipped with a frequency variable device are annularly connected. Is connected to a plurality of refrigerant separators having a functional film larger than the permeation ratio of other refrigerants, and permeates a reservoir that arbitrarily stores the refrigerant discharged from the refrigerant separators on the permeate side and the non-permeate side of the functional film. Side and non-permeate side, each of which is connected to the main circuit through an electromagnetic on-off valve and a pressure reducing device or a variable pressure reducing device to form a refrigerant composition ratio variable cycle, and temperature detecting means for detecting the indoor temperature, and this temperature detecting means. First comparing means for comparing the detected temperature by the means and the set temperature obtained by adding a certain value to the indoor set temperature, a first comparing means, a timer for measuring the elapsed time from the start of operation, and the measured value and set time of this timer Compare with When the temperature is less than the set temperature by the second comparing means and the first comparing means and is less than the set time by the second comparing means, the refrigerant other than the component with the lowest boiling point is stored in the reservoir. When the temperature is lower than the set temperature by the first comparing means and longer than the set time by the second comparing means, the refrigerant having the highest boiling point is stored in the reservoir. To the second output mode in which the refrigerant is switched so that the refrigerant having the lowest boiling point component is stored in the reservoir when the temperature is higher than the set temperature by the first comparing means. A refrigerating apparatus comprising a transfer means for transferring and an output means for outputting an electric signal to an electromagnetic on-off valve or a variable pressure reducing device according to the output mode.
【請求項2】温度検出手段による室内温度と室内設定温
度にある値を加えた設定温度との差が任意の値以上の場
合、最も高沸点の成分以外の冷媒が貯留器に貯留される
ように切り換える第4の出力モードに移行する移行手段
と前記出力モードにより電磁開閉弁もしくは可変式減圧
装置に電気信号を出力する出力手段を具備した請求項1
記載の冷凍装置。
2. A refrigerant other than the highest boiling point component is stored in the reservoir when the difference between the room temperature detected by the temperature detecting means and the set temperature obtained by adding a certain value to the room set temperature is equal to or more than an arbitrary value. 2. A transition means for transitioning to a fourth output mode for switching to the above, and an output means for outputting an electric signal to an electromagnetic on-off valve or a variable pressure reducing device according to the output mode.
The refrigeration system described.
【請求項3】周波数可変装置を具備した圧縮機、凝縮
機、主絞り装置、蒸発器を環状に接続した主回路に複数
種類の冷媒を封入した冷凍サイクルにおいて、特定の種
類の冷媒の透過割合が他の冷媒の透過割合より大きい機
能膜を有した冷媒分離装置を複数個接続し、前記機能膜
の透過側及び非透過側の冷媒分離装置より出た冷媒を任
意に貯留する貯留器を透過側、非透過側各々に電磁開閉
弁と減圧装置もしくは可変式減圧装置を介して前記主回
路に接続して冷媒組成比率可変サイクルを構成し、運転
開始からの時間経過を計測するタイマーとこのタイマー
の計測値と設定時間とを比較する第1の比較手段と、圧
縮機の運転周波数を検出する周波数検出手段と、この周
波数検出手段による検出周波数と設定周波数との大、小
とを比較する第2の比較手段と、前記第2の比較手段に
より設定周波数より大の場合で前記第1の比較手段によ
り設定時間より小の場合、最も低沸点の成分以外の冷媒
が貯留器に貯留されるように切り換える第1の出力モー
ドに、また前記第2の比較手段により設定周波数より大
の場合で前記第1の比較手段により設定時間より大の場
合、最も高沸点の成分の冷媒が貯留器に貯留されるよう
に切り換える第2の出力モードに、また前記第2の比較
手段により設定周波数より小の場合、最も低沸点の成分
の冷媒が貯留器に貯留されるように切り換える第3の出
力モードに移行する移行手段と前記出力モードにより電
磁開閉弁もしくは可変式減圧装置に電気信号を出力する
出力手段を具備した冷凍装置。
3. A permeation ratio of a specific type of refrigerant in a refrigeration cycle in which a plurality of types of refrigerant are enclosed in a main circuit in which a compressor, a condenser, a main expansion device, and an evaporator equipped with a frequency variable device are annularly connected. Is connected to a plurality of refrigerant separators having a functional film larger than the permeation ratio of other refrigerants, and permeates a reservoir that arbitrarily stores the refrigerant discharged from the refrigerant separators on the permeate side and the non-permeate side of the functional film. Of the refrigerant composition ratio variable cycle by connecting to the main circuit through a solenoid on-off valve and a pressure reducing device or a variable pressure reducing device on each of the side and the non-permeable side, and a timer for measuring the elapsed time from the start of operation and this timer No. 1 comparing means for comparing the measured value with the set time, frequency detecting means for detecting the operating frequency of the compressor, and first comparing means for comparing the detected frequency of the frequency detecting means with the set frequency. 2's When the frequency is higher than the set frequency by the comparing means and the second comparing means and is shorter than the set time by the first comparing means, the refrigerant other than the lowest boiling point component is stored in the reservoir. In the first output mode, and when the frequency is higher than the set frequency by the second comparison means and longer than the set time by the first comparison means, the refrigerant having the highest boiling point is stored in the reservoir. To the second output mode for switching to the above, and to the third output mode for switching so that the refrigerant having the lowest boiling point component is stored in the reservoir when the frequency is smaller than the set frequency by the second comparing means. A refrigeration system comprising a transition means and an output means for outputting an electric signal to an electromagnetic on-off valve or a variable pressure reducing device according to the output mode.
JP32660988A 1988-12-23 1988-12-23 Refrigeration equipment Expired - Fee Related JPH0760024B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32660988A JPH0760024B2 (en) 1988-12-23 1988-12-23 Refrigeration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32660988A JPH0760024B2 (en) 1988-12-23 1988-12-23 Refrigeration equipment

Publications (2)

Publication Number Publication Date
JPH02171556A JPH02171556A (en) 1990-07-03
JPH0760024B2 true JPH0760024B2 (en) 1995-06-28

Family

ID=18189718

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32660988A Expired - Fee Related JPH0760024B2 (en) 1988-12-23 1988-12-23 Refrigeration equipment

Country Status (1)

Country Link
JP (1) JPH0760024B2 (en)

Also Published As

Publication number Publication date
JPH02171556A (en) 1990-07-03

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